EP0079842B1 - Acrylic copolymers based on n-acrylylpolymethylene imines or n-acrylyldialkyl amides, n,n'-acrylyldiamino alcanes and n-acrylylamino acids (or esters), their preparation and their use as cation exchangers - Google Patents
Acrylic copolymers based on n-acrylylpolymethylene imines or n-acrylyldialkyl amides, n,n'-acrylyldiamino alcanes and n-acrylylamino acids (or esters), their preparation and their use as cation exchangers Download PDFInfo
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- EP0079842B1 EP0079842B1 EP82402110A EP82402110A EP0079842B1 EP 0079842 B1 EP0079842 B1 EP 0079842B1 EP 82402110 A EP82402110 A EP 82402110A EP 82402110 A EP82402110 A EP 82402110A EP 0079842 B1 EP0079842 B1 EP 0079842B1
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F220/00—Copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and only one being terminated by only one carboxyl radical or a salt, anhydride ester, amide, imide or nitrile thereof
- C08F220/02—Monocarboxylic acids having less than ten carbon atoms; Derivatives thereof
- C08F220/52—Amides or imides
- C08F220/54—Amides, e.g. N,N-dimethylacrylamide or N-isopropylacrylamide
- C08F220/56—Acrylamide; Methacrylamide
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F220/00—Copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and only one being terminated by only one carboxyl radical or a salt, anhydride ester, amide, imide or nitrile thereof
- C08F220/02—Monocarboxylic acids having less than ten carbon atoms; Derivatives thereof
- C08F220/52—Amides or imides
- C08F220/54—Amides, e.g. N,N-dimethylacrylamide or N-isopropylacrylamide
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J39/00—Cation exchange; Use of material as cation exchangers; Treatment of material for improving the cation exchange properties
- B01J39/08—Use of material as cation exchangers; Treatment of material for improving the cation exchange properties
- B01J39/16—Organic material
- B01J39/18—Macromolecular compounds
- B01J39/20—Macromolecular compounds obtained by reactions only involving unsaturated carbon-to-carbon bonds
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J39/00—Cation exchange; Use of material as cation exchangers; Treatment of material for improving the cation exchange properties
- B01J39/26—Cation exchangers for chromatographic processes
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- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07K—PEPTIDES
- C07K1/00—General methods for the preparation of peptides, i.e. processes for the organic chemical preparation of peptides or proteins of any length
- C07K1/04—General methods for the preparation of peptides, i.e. processes for the organic chemical preparation of peptides or proteins of any length on carriers
- C07K1/042—General methods for the preparation of peptides, i.e. processes for the organic chemical preparation of peptides or proteins of any length on carriers characterised by the nature of the carrier
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F8/00—Chemical modification by after-treatment
- C08F8/30—Introducing nitrogen atoms or nitrogen-containing groups
- C08F8/32—Introducing nitrogen atoms or nitrogen-containing groups by reaction with amines
Definitions
- the subject of the present invention is new crosslinked statistical acrylic copolymers which can be used in a very wide range of solvents (water, methylene chloride, chloroform, methanol, ethanol, dimethylformamide, pyridine, etc.), their preparation methods and their use in ion exchange chromatography.
- solvents water, methylene chloride, chloroform, methanol, ethanol, dimethylformamide, pyridine, etc.
- the technique of ion exchange chromatography consists of the use of an insoluble support (matrix) on which are fixed ionizable groups associated with ions of opposite signs (counterions).
- This technique is applicable to the separation of the different constituents of a mixture in solution; the non-ionized molecules will be eluted quickly, the ionized molecules will be more or less retained due to the exchange of ions occurring with the matrix.
- the present invention relates to new copolymers which can be used in particular as cation exchange resins.
- non-functional polymers prepared by radical copolymerization of derivatives of acrylic or methacrylic acid with a crosslinking agent which can be either methylene bis acrylamide (N, N'-diacryloyldiaminomethane, abbreviation MBA), or divinylbenzene.
- a crosslinking agent which can be either methylene bis acrylamide (N, N'-diacryloyldiaminomethane, abbreviation MBA), or divinylbenzene.
- the copolymer of acrylamide and of methylene bis acrylamide gives, after partial hydrolysis by soda, the support known under the trade mark Biogel 70 (Inman and Dintzis, "Biochemistry", 1969, 8, 4074).
- the use as a monomer serving as a mesh, of N-acrylylpolymethyleneimine 1 or of N-acrylyldialcoylamide 2, with disubstituted amide functions makes it possible to completely eliminate the intervention of the hydrogen bonds.
- the resins prepared have a high swelling rate in a wide range of organic solvents (protic and aprotic) and in aqueous buffers of various pH.
- copolymers in acid form are chemically stable in a clearly acidic or basic medium. Treatments lasting several days with solutions of hydrochloric acid or sodium hydroxide 0.5 and 1 M, at room temperature, have shown that no hydrolysis, even partial, takes place.
- copolymers are thermally stable; in fact, by heating at 90 ° C. for 12 h, under a vacuum of 0.1 mm of mercury, no change is observed.
- crosslinked copolymers according to the invention can be prepared, according to known methods, by radical polymerization of the monomers I, II and III.
- the aqueous solution containing the various monomers and the initiator is subjected to a polymerization in homogeneous phase.
- the transparent gel which forms is quickly ground, washed and sieved; this process gives a quantitative yield, in particular of copolymers of homogeneous size.
- the suspension polymerization directly supplies the resin in the form of spherical particles; these are washed with great care, dried. Their size is also very homogeneous; the diameter being between 0.1 and 0.25 mm (microscopic determination).
- an agent initiating the polymerization and the emulsifying agent are added to the homogeneous solution containing the various monomers.
- the whole is poured into an organic liquid phase, immiscible with water, kept stirring.
- the stirring speed is adjusted so as to obtain an emulsion having the desired droplet size.
- the polymerization is then initiated, either by addition of TMEDA, or by slight heating.
- the mixture is then stirred to completion; the resin beads obtained are washed with a hydrocarbon solvent, then with water, ethanol and ethyl ether.
- the resin is finally dried at room temperature under high vacuum.
- liquid organic phase which can be used, mention may, for example, be made of vegetable oils (soybean oil, peanut oil, sunflower oil, etc.) or mineral oils (paraffin oil, silicone oil).
- the emulsifying agent can be one of the products known under the trade name Span, Arlacel or Tween, at a concentration of 0.1 to 4% by volume.
- Identical polymerization conditions are used: from 15 g (0.12 mol) of AP, 1.31 g (7.8. 10 -3 mol) of EBA and 2.55 g (1.631. 10 - 2 mol) of methyl ester of N-acrylyl ⁇ alanine in 34.2 ml of ethanol and with the same quantities of water (18 ml), of phosphate buffer (pH 6.0) (21.6 ml) , ammonium persulfate (3.16 g) and TMEDA (0.53 ml), 9.43 g of dry resin are isolated after saponification under conditions identical to those described in the preceding paragraph and after sieving white.
- the pKa of the OH form is 4.8.
- N-acrylylpyrrolidine (0.12 mol, 15 g)
- EBA 0.0078 mol, 1.31 g
- N-acrylyl s aminocaproate methyl ester (16,31. 10 -3 mol, 3 g). 13 g (68%) of white, dry resin are thus isolated, after elimination of the fines.
- Copolymerization AP EBA, methyl ester of N-acrylyl L-leucine (abbreviation A (L) Leu O CH 3 ).
- the amounts of monomers used are: 15 g of N-acrylylpyrrolidine, 1.31 g of EBA, 3.24 g of methyl ester of N-acrylyl L-leucine.
- the dry ester resin (10.05 g) is hydrolyzed with 300 ml of molar sodium hydroxide. After treatment as indicated above and sieving, 8.49 g of acid resin are isolated. The pKa of the OH form is 4.8.
- N-acrylylmorpholine 5 g (0.0355 mol) of N-acrylylmorpholine, 0.38 g (0.0023 mol) of EBA and 0.995 g (5.38 . 10- 3 mol) of N-acrylyl ⁇ amino methyl caproate are dissolved in 10.4 ml of ethanol. After degassing with the sonicator, 6 ml of water, 7.2 ml of 0.1 M disodium phosphate buffer solution, 1.05 g of ammonium persulfate and 0.176 are successively added, under the conditions indicated in the first example. ml of TM EDA.
- the polymerization leads to 4.93 g (77.4%) of dry white resin.
- the hydrolysis provides, after sieving, 2.35 g of dry acid resin, the pKa of the OH form is 5.1.
- the polymerization is carried out under the conditions of the preceding paragraph, with 5 g (0.0355 mol) of N-acrylylmorpholine, 0.38 g (0.0023 mol) of EBA and 0.844 g (5.38.10 -3) as the monomer. mol) of methyl ester of N-acrylyl ⁇ alanine. 4.24 g (68.2%) of dry ester resin are thus isolated, giving, after hydrolysis and sieving, 2.18 g of dry acid resin. The pKa of the OH form is 4.8.
- ADM N, N-dimethylacrylamide
- EBA methyl ester of N-acrylyl ⁇ aminocaproic acid
- the polymerization is carried out from 4.653 g (0.047 mol) of N-dimethylacrylamide, 0.51 g (0.003 mol) of EBA and 0.81 g (5.16 . 10 -3 mol) of methyl ester of N-acrylyl ⁇ alanine.
- the polymerization is carried out from 2 g of N-diethylacrylamide, 0.17 g of EBA and 0.32 g of methyl ester of N-acrylyl alanine in 4.5 ml of ethanol, by successive additions of 2, 35 ml of water, 2.82 ml of 0.1 M disodium phosphate buffer, 0.42 g of ammonium persulfate and 0.067 ml of TM EDA. After hydrolysis and sieving, 1.31 g of dry acid resin are isolated. The pKa of OH form is 5.5.
- the resin is then sieved. The following size distribution is obtained:
- the reaction can also be carried out in water in place of the phosphate buffer.
- the sodium salts of acid resins are easily obtained by washing the polymers with 0.5M sodium hydroxide solutions. 30 ml of sodium hydroxide solution are used per milliliter of swollen acid resin. The excess soda is removed by washing with water until neutral.
- the particle size is between 0.1 and 0.25 mm.
- the charge in the carboxylic group is close to 0.8 mEq / g of dry resin.
- the chromatograms, fig. 1 and 2 below, show a very good separation between the components of the analyzed mixtures.
- Calf thymus histones were also chromatographed in a sodium chloride gradient (0 to 2M) (fig. 3). A resolution of the various components is observed, with a very short analysis time (5 h), a rapid flow rate (80 ml / h), and a buffer (NaCl) better suited to UV analysis.
- histone ion exchange chromatographies are carried out in gradients with elaborate forms of guanidinium chloride with very slow flow rates and analysis times which can vary between 12 h and several days (J. Bonner et al., "Method in Enzymology", vol. 126; Grossmann L. and Maldave K. Editeurs, Academic Press, New York, 1968).
- the resins according to the invention are therefore compatible with proteins and allow good separations to be easily carried out. It should also be noted that the supports described here admit very high bit rates. It is possible to work up to 300 ml / h with a 1 x 25 cm column.
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Abstract
Description
La présente invention a pour objet de nouveaux copolymères acryliques statistiques réticulés, utilisables dans une très large gamme de solvants (eau, chlorure de méthylène, chloroforme, méthanol, éthanol, diméthylformamide, pyridine, etc.), leurs procédés de préparation et leur emploi dans la chromatographie d'échange d'ions.The subject of the present invention is new crosslinked statistical acrylic copolymers which can be used in a very wide range of solvents (water, methylene chloride, chloroform, methanol, ethanol, dimethylformamide, pyridine, etc.), their preparation methods and their use in ion exchange chromatography.
La technique de la chromatographie d'échange d'ions consiste en l'emploi d'un support insoluble (matrice) sur lequel sont fixés des groupes ionisa- bles associés à des ions de signes contraires (contre-ions).The technique of ion exchange chromatography consists of the use of an insoluble support (matrix) on which are fixed ionizable groups associated with ions of opposite signs (counterions).
Ces derniers peuvent être échangés avec d'autres ions de même signe, contenus dans une phase mobile que l'on met en contact avec la matrice. Selon le caractère acide ou basique des groupes fixés, on parlera d'une résine échangeuse de cations ou d'anions.These can be exchanged with other ions of the same sign, contained in a mobile phase which is brought into contact with the matrix. Depending on the acidic or basic character of the fixed groups, we will speak of a cation or anion exchange resin.
Cette technique est applicable à la séparation des différents constituants d'un mélange en solution; les molécules non ionisées serontéluées rapidement, les molécules ionisées seront plus ou moins retenues en raison de l'échange d'ions intervenant avec la matrice.This technique is applicable to the separation of the different constituents of a mixture in solution; the non-ionized molecules will be eluted quickly, the ionized molecules will be more or less retained due to the exchange of ions occurring with the matrix.
La présente invention concerne de nouveaux copolymères utilsables notamment comme résines échangeuses de cations.The present invention relates to new copolymers which can be used in particular as cation exchange resins.
Il existe actuellement un certain nombre de résines acryliques ou méthacryliques, possédant des groupes acides carboxyliques, qui sont utilisées comme support en chromatographie d'échange d'ions (échangeurs de cations).There are currently a number of acrylic or methacrylic resins, having carboxylic acid groups, which are used as a support in ion exchange chromatography (cation exchangers).
Elles sont généralement obtenues à partir de polymères non fonctionnels, préparées par copolymérisation radicalaire de dérivés de l'acide acrylique ou méthacrylique avec un agent de réticulation qui peut être soit le méthylène bis acrylamide (N,N'-diacryloyldiaminométhane, abréviation MBA), soit le divinylbenzène.They are generally obtained from non-functional polymers, prepared by radical copolymerization of derivatives of acrylic or methacrylic acid with a crosslinking agent which can be either methylene bis acrylamide (N, N'-diacryloyldiaminomethane, abbreviation MBA), or divinylbenzene.
Dans la majorité des cas, les fonctions acides sont alors introduites dans la matrice par des modifications chimiques intervenant après la polymérisation. Ces réactions sont difficiles à contrôler et peuvent conduire à un manque d'homogénéité au niveau de la fonctionnalisation (hydrolyse de la maille ou de l'agent de réticulation).In the majority of cases, the acid functions are then introduced into the matrix by chemical modifications occurring after the polymerization. These reactions are difficult to control and can lead to a lack of homogeneity in terms of functionalization (hydrolysis of the mesh or of the crosslinking agent).
Ainsi, le copolymère d'acrylamide et de méthylène bis acrylamide (connu sous la marque commerciale Biogel P appartenant à Biorad Laborato- ries) donne, après hydrolyse partielle par la soude, le support connu sous la marque commerciale Biogel 70 (Inman et Dintzis, «Biochemistry», 1969, 8, 4074).Thus, the copolymer of acrylamide and of methylene bis acrylamide (known under the trade name Biogel P belonging to Biorad Laboratories) gives, after partial hydrolysis by soda, the support known under the trade mark Biogel 70 (Inman and Dintzis, "Biochemistry", 1969, 8, 4074).
Il ressort de la structure chimique de ces résines (figure ci-dessous) que la fonction carboxylique est adjacente à la chaîne du polymère; par conséquent, des contraintes stériques gêneront l'interaction entre des molécules volumineuses et le site acide.
La même critique peut être formulée à l'encontre d'autres résines comme celles connues sous la marque commerciale Trisacryl appartenant à Pharmindustrie (brevets français Nos 2378808 et 2482112), qui, elles, sont obtenues par la copolymérisation avec un monomère fonctionnalisé.The same criticism can be made against other resins such as those known under the trademark Trisacryl belonging to Pharmindustrie (French patents Nos 2378808 and 2482112), which are obtained by copolymerization with a functionalized monomer.
En outre, certains gels de polyacrylamide (Biogel, Duolite) sont chimiquement instables en milieu basique du fait de l'hydrolyse des groupes amides en groupes carboxyliques, ce qui limite leur domaine d'emploi (Inman et Dintzis, déjà cité).In addition, certain polyacrylamide gels (Biogel, Duolite) are chemically unstable in basic medium due to the hydrolysis of amide groups into carboxylic groups, which limits their field of use (Inman and Dintzis, already cited).
Il faut noter également les limitations introduites par le manque de stabilité mécanique des polyacrylamides à fonction amide primaire (Scouten, «Affinity Chromatography: bioselective absorption on inert matrices», Wiley, 1981).Note also the limitations introduced by the lack of mechanical stability of polyacrylamides with primary amide function (Scouten, "Affinity Chromatography: bioselective absorption on inert matrices", Wiley, 1981).
On peut, enfin, mentionner une résine décrite par Sheppard et coll. («J.C.S. Perkin Trans I», 1981, pp. 529 et 538), résultant de la copolymérisation du N-acrylyldiméthylamide, du N,N'-di- acrylyldiamino-1, 2-éthane et de l'ester méthylique de la N-acrylylsarcosine. Cependant, ce support n'a jamais été hydrolysé en copolymère de N-acrylyldiméthylamide, N,N'-diacrylyldiamino-1, 2 éthane et N-acrylylsarcosine, pour être utilisé en tant qu'échangeur de cation. Si l'on effectue cette transformation et teste la résine acide ainsi obtenue, en chromatographie d'échange d'ions, on constate des variations de volume très importantes en fonction de la force ionique de l'éluant. Ainsi, en travaillant avec des solutions de chlorure de sodium de concentration progressive comprise entre 0 et 0,5 M, on peut noter une contraction de volume supérieure à 50% du support de Sheppard hydrolysé; cela induit un volume mort important et, par là même, une forte incertitude sur la valeur du gradient d'élution; d'où l'utilisation délicate de ce type de support en chromatographie d'échange de cations.Finally, mention may be made of a resin described by Sheppard et al. ("JCS Perkin Trans I", 1981, pp. 529 and 538), resulting from the copolymerization of N-acrylyldimethylamide, N, N'-di-acrylyldiamino-1, 2-ethane and the methyl ester of N -acrylylsarcosine. However, this support has never been hydrolyzed to a copolymer of N-acrylyldimethylamide, N, N'-diacrylyldiamino-1, 2 ethane and N-acrylylsarcosine, to be used as a cation exchanger. If this transformation is carried out and the acid resin thus obtained is tested, in ion exchange chromatography, very large volume variations are observed as a function of the ionic strength of the eluent. Thus, by working with sodium chloride solutions of progressive concentration between 0 and 0.5 M, it is possible to note a volume contraction greater than 50% of the hydrolyzed Sheppard support; this induces a large dead volume and, thereby, a high uncertainty about the value of the elution gradient; hence the delicate use of this type of support in cation exchange chromatography.
Afin de proposer un nouveau type de copolymère ne présentant pas les inconvénients de ceux déjà connus, il a été mis au point, conformément à la présente invention, un nouveau type polyvalent de copolymères statistiques réticulés, par copolymérisation de trois monomères distincts définis comme suit:
- I. Un monomère défini comme étant la maille du support et qui consiste en une N-acrylylpolyméthylèneimine de formule:
- II. Un monomère défini comme étant l'agent de réticulation et qui consiste en un N,N'-bis- acrylyldiaminoalcane de formule:
- III. Un monomère défini comme étant l'agent de fonctionnalisation et qui consiste en un N-acrylylaminoacide ou ester, de formule:
- R, = H ou-CH3
- R3 = H ou -CH3
- n3=1,2,3 ou5
ou un N-acrylylaminoacide (ou ester) asymétrique de série L, de formule: * - R1 = H ou -CH3
- R3 ayant la signification précédente
- R4 = -CH3
- R1 = H ou -CH3
- R3 ayant la signification précédente.
- I. A monomer defined as being the mesh of the support and which consists of an N-acrylylpolymethyleneimine of formula:
- II. A monomer defined as being the crosslinking agent and which consists of an N, N'-bis-acrylyldiaminoalkane of formula:
- III. A monomer defined as being the functionalizing agent and which consists of an N-acrylylamino acid or ester, of formula:
- R, = H ou-CH 3
- R 3 = H or -CH 3
- n 3 = 1,2,3 or 5
or an asymmetric N-acrylylamino acid (or ester) of series L, of formula: * - R 1 = H or -CH 3
- R 3 having the previous meaning
- R4 = -CH 3
- R 1 = H or -CH 3
- R 3 having the previous meaning.
L'utilisation comme monomère servant de maille, de N-acrylylpolyméthylèneimine 1 ou de N-acrylyldialcoylamide 2, avec des fonctions amides disubstituées, permet de supprimer totalement l'intervention des liaisons hydrogène. Aussi, les résines préparées ont un fort taux de gonflement dans une large gamme de solvants organiques (protiques et aprotiques) et dans des tampons aqueux de divers pH.The use as a monomer serving as a mesh, of N-acrylylpolymethyleneimine 1 or of N-acrylyldialcoylamide 2, with disubstituted amide functions, makes it possible to completely eliminate the intervention of the hydrogen bonds. Also, the resins prepared have a high swelling rate in a wide range of organic solvents (protic and aprotic) and in aqueous buffers of various pH.
La fonctionnalisation des supports, réalisée par l'emploi de N-acrylylaminoacides (ou esters) 4, 5 ou 6, rend possible la modification de la nature et de la longueur du bras séparant la fonction acide ou ester du squelette polymérique.The functionalization of the supports, carried out by the use of N-acrylylamino acids (or esters) 4, 5 or 6, makes it possible to modify the nature and the length of the arm separating the acid or ester function from the polymer backbone.
Certains monomères intervenant dans la maille sont connus. Ils ont été décrits, avec leurs procédés de préparation, dans diverses publications parmi lesquelles:
- Composés 1: R1 = H, Z = -(CH2)4-, -(CH2)5-Z -(CH2)2-O-(CH2)2-Parrod et coll., «J. Polymer. Sci.»,1958, 29,111.
- Composés 2: R, = H, R2 = -cH3
- Ratchford et coll., «J. Amer. Chem. Soc.», 1947, 69, 1911.
- R1 = H, R2 = -C2H5,
- Brevet américain No 2683741.
- Compounds 1: R 1 = H, Z = - (CH 2 ) 4-, - (CH 2 ) 5-Z - (CH 2 ) 2 -O- (CH 2 ) 2 -Parrod et al., "J. Polymer. Sci. ”, 1958, 29,111.
- Compounds 2: R, = H, R 2 = -cH 3
- Ratchford et al., "J. Bitter. Chem. Soc. ”, 1947, 69, 1911.
- R1 = H , R2 = -C 2 H 5 ,
- US Patent No. 2,683,741.
Composés 3:
- Les agents de formule 3 sont connus:
- n2 = 1 (commercial)
- n2 = 2
- Sheppard et coll., «J. Chem. Soc. Perkin I», 1981, 529.
- The agents of formula 3 are known:
- n 2 = 1 (commercial)
- n 2 = 2
- Sheppard et al., "J. Chem. Soc. Perkin I ", 1981, 529.
Enfin, certains agents de fonctionnalisation de formule 4, 5 ou 6 ont été décrits dans la littérature.Finally, certain functionalizing agents of formula 4, 5 or 6 have been described in the literature.
Composés 4:
- Brown et coll., «C.R. Acad. Sci.», 1978, 287c, 125.
- R1=CH3,R3=H,n3=1,2,3 ou5
- Batz et Koldehoff, «Makromol. Chem.», 1976, 177,683.
- Brown et al., "CR Acad. Sci. ”, 1978, 287c, 125.
- R 1 = CH 3 , R 3 = H, n 3 = 1,2,3 or5
- Batz and Koldehoff, "Makromol. Chem. ”, 1976, 177,683.
Winston et Kirchner, «Macromolécules», 1978, 11, 89.Winston and Kirchner, "Macromolecules", 1978, 11, 89.
Loupek et coll., «Bioch. Biophys. Act.», 1977, 481, 289.Loupek et al., "Bioch. Biophys. Act. ”, 1977, 481, 289.
Composés 5:
Sakota, «Koine Nippon Zagakin Zashi», 1967, 88 (10), 1087.Sakota, "Koine Nippon Zagakin Zashi", 1967, 88 (10), 1087.
La copolymérisation de ces deux catégories de monomères I d'une part, III, d'autre part, utilisés respectivement en tant que maille et agent de fonctionnalisation, avec un agent de réticulation de type II, permet d'obtenir des résines ayant des comportements physiques compatibles avec les chromatographies d'échange d'ions, en particulier en ce qui concerne le débit d'élution. Ainsi, les contractions de volume en fonction de la force ionique de l'éluant aqueux n'ont jamais été supérieures à 15%.The copolymerization of these two categories of monomers I on the one hand, III, on the other hand, used respectively as mesh and functionalizing agent, with a type II crosslinking agent, makes it possible to obtain resins having behaviors compatible with Ion exchange chromatographies, in particular with regard to the elution rate. Thus, the volume contractions as a function of the ionic strength of the aqueous eluent have never been greater than 15%.
Les conditions de polymérisation étant parfaitement contrôlées et les rendements élevés, il est possible de faire varier dans une large gamme le taux de fonctionnalisation. Pour cela, il suffit de modifier la quantité relative de N-acrylylaminoacide (ou ester) III, par rapport aux deux autre monomères.The polymerization conditions being perfectly controlled and the yields high, it is possible to vary over a wide range the functionalization rate. To do this, it suffices to modify the relative amount of N-acrylylamino acid (or ester) III, with respect to the two other monomers.
Les copolymères selon l'invention sont des copolymères statistiques réticulés tridimensionnels, contenant sous forme copolymérisée:
- a) de 30 à 90% en poids d'un monomère correspondant à une N-acrylylpolyméthylèneimine de formule 1 ou à un N-acrylyldialcoylamide de formule 2;
- b) de 2 à 50% en poids d'un monomère correspondant à un N,N'-diacrylyldiaminoalcane de formule 3;
- c) de 2 à 65% en poids d'un monomère correspondant à un acrylylaminoacide ou ester, racémique de formule 4 ou optiquement actif de formule 5 ou 6.
- a) from 30 to 90% by weight of a monomer corresponding to an N-acrylylpolymethyleneimine of formula 1 or to an N-acrylyldialcoylamide of formula 2;
- b) from 2 to 50% by weight of a monomer corresponding to an N, N'-diacrylyldiaminoalkane of formula 3;
- c) from 2 to 65% by weight of a monomer corresponding to an acrylylamino acid or ester, racemic of formula 4 or optically active of formula 5 or 6.
Les copolymères selon l'invention contiennent de préférence:
- - de 70 à 90% de monomère 1 (définissant la maille) correspondant aux formules 1 et 2;
- - de 3 à 10% de monomère Il (agent de réticulation) correspondant à la formule 3;
- - de 10 à 20% de monomère III (agent de fonctionnalisation) correspondant aux formules 4, 5 et 6.
- - from 70 to 90% of monomer 1 (defining the mesh) corresponding to formulas 1 and 2;
- - from 3 to 10% of monomer II (crosslinking agent) corresponding to formula 3;
- - from 10 to 20% of monomer III (functionalizing agent) corresponding to formulas 4, 5 and 6.
Selon l'invention on a pu préparer des supports contenant de 0,2 à 10 mEq en groupe carboxylique par gramme de support sec (directement ou après saponification). Il a été noté, d'autre part, qu'aucune hydrolyse de la fonction ester n'intervient lors de la polymérisation.According to the invention, it was possible to prepare supports containing from 0.2 to 10 mEq in carboxylic group per gram of dry support (directly or after saponification). It has been noted, on the other hand, that no hydrolysis of the ester function takes place during the polymerization.
Les copolymères sous forme acide sont chimiquement stables en milieu nettement acide ou basique. Des traitements de plusieurs jours, par des solutions d'acide chlorhydrique ou de soude 0,5 et 1 M, à température ambiante, ont montré qu'aucune hydrolyse, même partielle, n'intervenait.The copolymers in acid form are chemically stable in a clearly acidic or basic medium. Treatments lasting several days with solutions of hydrochloric acid or sodium hydroxide 0.5 and 1 M, at room temperature, have shown that no hydrolysis, even partial, takes place.
Cela est lié à la présence, sur le monomère formant la maille, d'un amide secondaire relativement encombré, beaucoup plus stable que les amides primaires généralement utilisés. Cela permet l'emploi de nos supports dans un domaine de pH très étendu (1 à 14). Les résines obtenues présentent des pK variant de 4,5 à 5,0.This is linked to the presence, on the monomer forming the mesh, of a relatively hindered secondary amide, much more stable than the primary amides generally used. This allows the use of our supports in a very wide pH range (1 to 14). The resins obtained have pK ranging from 4.5 to 5.0.
Ces copolymères sont stables thermiquement; en effet, par chauffage à 90° C pendant 12 h, sous vide de 0,1 mm de mercure, on ne constate aucune modification.These copolymers are thermally stable; in fact, by heating at 90 ° C. for 12 h, under a vacuum of 0.1 mm of mercury, no change is observed.
Enfin, ces supports présentent une excellente stabilité mécanique. Après agitation mécanique pendant plusieurs jours, on ne constate pas de formation de fines (aucune turbidité dans le liquide surnageant).Finally, these supports have excellent mechanical stability. After mechanical stirring for several days, there is no formation of fines (no turbidity in the supernatant).
Les copolymères réticulés selon l'invention peuvent être préparés, selon des procédés connus, par polymérisation radicalaire des monomères I, Il et III.The crosslinked copolymers according to the invention can be prepared, according to known methods, by radical polymerization of the monomers I, II and III.
La copolymérisation peut en particulier être effectuée soit en bloc, dans un mélange alcool éthy- lique/eau ou diméthylformamide/eau en milieu tamponné (pH = 6,0), soit en suspension dans les systèmes eau/paraffine ou alcool polyvinyli- que/eau. L'amorçage est réalisé par les initiateurs habituellement utilisés en polymérisation radicalaire. Comme tels, on peut citer:
- - les couples comme N,N,N',N'-tétraméthyl- éthylènediamine (TMEDA) + persulfate alcalin,
- - le persulfate d'ammonium,
- - ou encore l'azo-isobutyronitrile.
- - couples such as N, N, N ', N'-tetramethyl-ethylenediamine (TMEDA) + alkaline persulfate,
- - ammonium persulfate,
- - or even azo-isobutyronitrile.
On utilise de 3 à 10% du poids d'agent de réticulation et une quantité d'agent de fonctionnalisation calculée de façon à obtenir 0,2 à 5 mEq de fonction acide carboxylique par gramme de résine sèche (directement ou après saponification); le complément à 100% en poids est constitué par le monomère destiné à constituer la maille.3 to 10% of the weight of crosslinking agent is used and an amount of functionalizing agent calculated so as to obtain 0.2 to 5 mEq of carboxylic acid function per gram of dry resin (directly or after saponification); the balance to 100% by weight consists of the monomer intended to constitute the mesh.
Dans le cas de la polymérisation en bloc, la solution aqueuse contenant les différents monomères et l'initiateur est soumise à une polymérisation en phase homogène. Le gel transparent qui se forme est rapidement broyé, lavé et tamisé; ce procédé donne un rendement quantitatif, en particulier de copolymères de taille homogène.In the case of block polymerization, the aqueous solution containing the various monomers and the initiator is subjected to a polymerization in homogeneous phase. The transparent gel which forms is quickly ground, washed and sieved; this process gives a quantitative yield, in particular of copolymers of homogeneous size.
La polymérisation en suspension fournit directement la résine sous forme de particules sphériques; celles-ci sont lavées avec beaucoup de soin, séchées. Leurtaille est aussi très homogène; le diamètre étant compris entre 0,1 et 0,25 mm (détermination microscopique).The suspension polymerization directly supplies the resin in the form of spherical particles; these are washed with great care, dried. Their size is also very homogeneous; the diameter being between 0.1 and 0.25 mm (microscopic determination).
Dans ce cas, à la solution homogène contenant les différents monomères, on ajoute un l'agent initiateur de la polymérisation et l'agent émulsifiant.In this case, to the homogeneous solution containing the various monomers, an agent initiating the polymerization and the emulsifying agent are added.
L'ensemble est versé dans une phase liquide organique, non miscible à l'eau, maintenue sous agitation. La vitesse d'agitation est réglée de façon à obtenir une émulsion ayant la taille de gouttelettes voulue. La polymérisation est alors initiée, soit par addition de TMEDA, soit par un léger chauffage.The whole is poured into an organic liquid phase, immiscible with water, kept stirring. The stirring speed is adjusted so as to obtain an emulsion having the desired droplet size. The polymerization is then initiated, either by addition of TMEDA, or by slight heating.
Le mélange est ensuite agité jusqu'à son terme; les perles de résines obtenues sont lavées avec un solvant hydrocarboné, puis à l'eau, à l'éthanol et à l'éther éthylique. La résine est finalement séchée à température ambiante sous vide poussé.The mixture is then stirred to completion; the resin beads obtained are washed with a hydrocarbon solvent, then with water, ethanol and ethyl ether. The resin is finally dried at room temperature under high vacuum.
Comme phase organique liquide, utilisable, on peut citer par exemple les huiles végétales (huile de soja, huile d'arachide, huile de tournesol, etc.) ou minérales (huile de paraffine, huile de silicone).As liquid organic phase which can be used, mention may, for example, be made of vegetable oils (soybean oil, peanut oil, sunflower oil, etc.) or mineral oils (paraffin oil, silicone oil).
L'agent émulsifiant peut être l'un des produits connus sous la dénomination commerciale Span, Arlacel ou Tween, à la concentration de 0,1 à 4% en volume.The emulsifying agent can be one of the products known under the trade name Span, Arlacel or Tween, at a concentration of 0.1 to 4% by volume.
Des exemples ci-après illustrent les différentes techniques de polymérisation ainsi que les différentes résines revendiquées dans la présente invention, sans la limiter.Examples below illustrate the various polymerization techniques as well as the various resins claimed in the present invention, without limiting it.
Copolymérisation d'acrylylpyrrolidine (abréviation AP), de l'éthylène bis acrylamide, encore appelé N,N'-diacrylyldiamino-9,2 éthane (abréviation EBA) et de l'ester méthylique de la N-acrylylglycine (abréviation A Gly 0 CH3).Copolymerization of acryllypyrrolidine (abbrevia tion AP), ethylene bis acrylamide, also called N, N'-diacrylyldiamino-9.2 ethane (abbreviation EBA) and the methyl ester of N-acrylylglycine (abbreviation A Gly 0 CH 3 ).
On dissout 0,12 mol (15 g) d'AP, 7,8.10-3 mol (1,31 g) d'EBA et 1,631 .10-2mol (2,33 g) d'ester méthylique de la N-acrylylglycine dans 34,2 ml d'éthanol anhydre. La solution incolore est dégazée 2 min au sonicateur. Par addition de 18 ml d'eau, la solution devient opaque. On laisse dégazer encore 2 min et on ajoute 21,6 ml de tampon phosphate (pH 6,0). Le dégazage est poursuivi jusqu'à retour à une solution limpide. On ajoute alors 3,16 g de persulfate d'ammonium et laisse dissoudre en dégazant. On ajoute alors 0,53 ml de TMEDA (N,N,N',N'-tétraméthyldiamino-1,2 éthane). Il se produit rapidement une élévation de température et la solution se prend en un gel transparent. On abandonne 0,5 h. Après broyage au broyeur Thomas, on laisse décanter dans l'eau afin d'éliminer les fines surnageantes. Cette opération est répétée une deuxième fois. Après filtration, la résine est successivement lavée avec de l'eau, un mélange eau/acétone 50/50 de l'acétone et finalement à l'éther. La poudre blanche obtenue est séchée 12 h à 80° C sous (2 mm) 2,66 mbar. On isole ainsi 13,86 g de résine blanche..Rdt 74,4%.0.12 mol (15 g) of AP, 7.8 × 10 -3 mol (1.31 g) of EBA and 1.631 are dissolved . 10 -2 mol (2.33 g) of methyl ester of N-acrylylglycine in 34.2 ml of anhydrous ethanol. The colorless solution is degassed for 2 min using a sonicator. By adding 18 ml of water, the solution becomes opaque. Leave to degas for another 2 min and add 21.6 ml of phosphate buffer (pH 6.0). The degassing is continued until return to a clear solution. 3.16 g of ammonium persulfate are then added and the solution is left to dissolve while degassing. 0.53 ml of TMEDA (N, N, N ', N'-tetramethyldiamino-1,2 ethane) is then added. There is a rapid rise in temperature and the solution becomes a transparent gel. We give up 0.5 h. After grinding in the Thomas grinder, it is left to settle in water in order to remove the supernatants. This operation is repeated a second time. After filtration, the resin is successively washed with water, a 50/50 water / acetone mixture of acetone and finally with ether. The white powder obtained is dried for 12 h at 80 ° C under (2 mm) 2.66 mbar. 13.86 g of white resin are thus isolated. Yield 74.4%.
Pour transformer cette résine ester en résine acide, on place les 13,86 g précédemment obtenus dans 300 ml de soude molaire et on agite pendant 2 h à 25° C. Après filtration la résine est lavée successivement l'eau,à à l'acide chlorhydrique (10%), à l'eau jusqu'à neutralité, à la soude molaire (500 ml), à l'eau jusqu'à neutralité, à l'acide chlorhydrique (10%), et finalement à l'eau jusqu'à neutralité. On sèche comme précédemment à 80° C sous 2 mm de mercure. Après tamisage pour éliminer les particules dont le diamètre est supérieur à 0,25 mm, on obtient 8,8 g de poudre blanche. Le pKa de la forme OH est de 4,4.To transform this ester resin into an acid resin, place the 13.86 g previously obtained in 300 ml of molar sodium hydroxide and stir for 2 h at 25 ° C. After filtration the resin is washed successively with water, at hydrochloric acid (10%), water until neutral, molar soda (500 ml), water until neutral, hydrochloric acid (10%), and finally water until neutral. Dry as above at 80 ° C under 2 mm of mercury. After sieving to remove particles with a diameter greater than 0.25 mm, 8.8 g of white powder are obtained. The pKa of the OH form is 4.4.
Des conditions identiques de polymérisation sont utilisées: à partir de 15 g (0,12 mol) d'AP, 1,31 g (7,8 .10-3 mol) d'EBA et 2,55 g (1,631. 10-2 mol) d'ester méthylique de la N-acrylyl β alanine dans 34,2 ml d'éthanol et avec les mêmes quantités d'eau (18 ml), de tampon phosphate (pH 6,0) (21,6 ml), de persulfate d'ammonium (3,16 g) et de TMEDA (0,53 ml), on isole, après saponification dans des conditions identiques à celles décrites dans le paragraphe précédent et après tamisage, 9,43 g de résine sèche et blanche. Le pKa de la forme OH est 4,8.Identical polymerization conditions are used: from 15 g (0.12 mol) of AP, 1.31 g (7.8. 10 -3 mol) of EBA and 2.55 g (1.631. 10 - 2 mol) of methyl ester of N-acrylyl β alanine in 34.2 ml of ethanol and with the same quantities of water (18 ml), of phosphate buffer (pH 6.0) (21.6 ml) , ammonium persulfate (3.16 g) and TMEDA (0.53 ml), 9.43 g of dry resin are isolated after saponification under conditions identical to those described in the preceding paragraph and after sieving white. The pKa of the OH form is 4.8.
Les mêmes conditions de polymérisation que dans les paragraphes précédents sont utilisées à partir des monomères suivants: N-acrylylpyrrolidine (0,12 mol, 15 g), EBA (0,0078 mol,1,31 g) et N-acrylyl s aminocaproate de méthyle (16,31. 10-3 mol, 3 g). On isole ainsi, après élimination des fines, 13 g (68%) de résine blanche et sèche.The same polymerization conditions as in the preceding paragraphs are used from the following monomers: N-acrylylpyrrolidine (0.12 mol, 15 g), EBA (0.0078 mol, 1.31 g) and N-acrylyl s aminocaproate methyl ester (16,31. 10 -3 mol, 3 g). 13 g (68%) of white, dry resin are thus isolated, after elimination of the fines.
L'hydrolyse dans les mêmes conditions que précédemment conduit, après tamisage, à 10,6 g de résine acide sèche et blanche. Le pKa de la forme OH est 5,1.Hydrolysis under the same conditions as above leads, after sieving, to 10.6 g of dry, white acid resin. The pKa of the OH form is 5.1.
A partir de 15 g (0,12 mol) de AP, 1,31 g (7,8 - 10-3 mol) de EBA et 2,76 g (0,01631 mol) d'ester méthylique de l'acide N-acrylyl y amino butyrique, on isole 12 g de résine ester sèche. Après hydrolyse dans 300 ml de soude molaire, on obtient par tamisage 10,8 g de résine acide sèche. Le pKa de la forme OH est 5,0.From 15 g (0.12 mol) of AP, 1.31 g (7.8 - 10- 3 mol) of EBA and 2.76 g (0.01631 mol) of N acid methyl ester -acrylyl y amino butyrique, 12 g of dry ester resin are isolated. After hydrolysis in 300 ml of molar sodium hydroxide, 10.8 g of dry acid resin are obtained by sieving. The pKa of the OH form is 5.0.
Les quantités de monomères utilisées sont: 15 g de N-acrylylpyrrolidine, 1,31 g de EBA, 3,24 g d'ester méthylique de la N-acrylyl L-leucine.The amounts of monomers used are: 15 g of N-acrylylpyrrolidine, 1.31 g of EBA, 3.24 g of methyl ester of N-acrylyl L-leucine.
La résine ester sèche (10,05 g) est hydrolysée par 300 ml de soude molaire. Après traitement comme indiqué précédemment et tamisage, on isole 8,49 g de résine acide. Le pKa de la forme OH est 4,8.The dry ester resin (10.05 g) is hydrolyzed with 300 ml of molar sodium hydroxide. After treatment as indicated above and sieving, 8.49 g of acid resin are isolated. The pKa of the OH form is 4.8.
On emploie 15 g de N-acrylylpyrrolidine, 1,31 g de EBA et 3 g d'ester méthylique de la N-acrylyl L-valine. La polymérisation et les traitements habituels donnent 9,96 g de résine ester sèche. L'hydrolyse par 300 ml de soude molaire conduit, dans les mêmes conditions que ci-dessus, à 7,64 g de résine acide blanche et sèche. Le pKa de la forme OH est 5,0.15 g of N-acrylylpyrrolidine, 1.31 g of EBA and 3 g of methyl ester of N-acrylyl L-valine are used. The polymerization and the usual treatments give 9.96 g of dry ester resin. Hydrolysis with 300 ml of molar sodium hydroxide leads, under the same conditions as above, to 7.64 g of white and dry acid resin. The pKa of the OH form is 5.0.
A partir de 15 g (0,12 mol) de N-acrylylpyrrolidine, 1,31 g (0,0078 mol de EBA) et 2,98 g d'ester méthylique de la N-acrylyl L-proline (16,31 10-3 mol), on isole 15,03 g (77,7%) de résine sèche. L'hydrolyse dans 300 ml de soude molaire conduit, après tamisage, à 11 g de résine acide sèche. Le pKa de la forme OH est 4,7.From 15 g (0.12 mol) of N-acrylylpyrrolidine, 1.31 g (0.0078 mol of EBA) and 2.98 g of methyl ester of N-acrylyl L-proline (16.31 10 -3 mol), 15.03 g (77.7%) of dry resin are isolated. Hydrolysis in 300 ml of molar soda leads, after sieving, to 11 g of dry acid resin. The pKa of the OH form is 4.7.
5 g (0,0355 mol) de N-acrylylmorpholine, 0,38 g (0,0023 mol) de EBA et 0,995 g (5,38. 10-3 mol) de N-acrylyl ε amino caproate de méthyle sont dissous dans 10,4 ml d'éthanol. Après dégazage au sonicateur, on ajoute successivement, dans les conditions indiquées dans le premier exemple, 6 ml d'eau, 7,2 ml de solution tampon de phosphate disodique 0,1 M, 1,05 g de persulfate d'ammonium et 0,176 ml de TM EDA.5 g (0.0355 mol) of N-acrylylmorpholine, 0.38 g (0.0023 mol) of EBA and 0.995 g (5.38 . 10- 3 mol) of N-acrylyl ε amino methyl caproate are dissolved in 10.4 ml of ethanol. After degassing with the sonicator, 6 ml of water, 7.2 ml of 0.1 M disodium phosphate buffer solution, 1.05 g of ammonium persulfate and 0.176 are successively added, under the conditions indicated in the first example. ml of TM EDA.
La polymérisation conduit à 4,93 g (77,4%) de résine sèche et blanche. L'hydrolyse fournit, après tamisage, 2,35 g de résine acide sèche, le pKa de la forme OH est 5,1.The polymerization leads to 4.93 g (77.4%) of dry white resin. The hydrolysis provides, after sieving, 2.35 g of dry acid resin, the pKa of the OH form is 5.1.
La polymérisation est effectuée dans les conditions du paragraphe précédent, avec comme monomère 5 g (0,0355 mol) de N-acrylylmorpholine, 0,38 g (0,0023 mol) de EBA et 0,844 g (5,38,10-3 mol) d'ester méthylique de la N-acrylyl β alanine. On isole ainsi 4,24 g (68,2%) de résine ester sèche, donnant, après hydrolyse et tamisage, 2,18 g de résine acide sèche. Le pKa de la forme OH est 4,8.The polymerization is carried out under the conditions of the preceding paragraph, with 5 g (0.0355 mol) of N-acrylylmorpholine, 0.38 g (0.0023 mol) of EBA and 0.844 g (5.38.10 -3) as the monomer. mol) of methyl ester of N-acrylyl β alanine. 4.24 g (68.2%) of dry ester resin are thus isolated, giving, after hydrolysis and sieving, 2.18 g of dry acid resin. The pKa of the OH form is 4.8.
4,653 g (0,047 mol) de N,N-diméthylacrylamide, 0,51 g (0,003 mol) de EBA et 0,955 g (5,16.10-3 mol) de N-acrylyl ε aminocaproate de méthyle sont dissous dans 13,4 ml d'alcool éthylique. Après dégazage au sonicateur, on ajoute successivement, dans les conditions déjà indiquées, 7,05 ml d'eau, 8,46 ml de solution tampon de phosphate disodique 0,1 M, 1,237 g de persulfate d'ammonium et 0,2 ml de TMEDA. On obtient 4,64 g (73%) de résine ester blanche, donnant après hydrolyse et tamisage 2,44 g de résine acide. Le pKa de la forme OH est 5,0.4.653 g (0.047 mol) of N, N-dimethylacrylamide, 0.51 g (0.003 mol) of EBA and 0.955 g (5.16. 10 -3 mole) of N-ε acrylyl methyl aminocaproate are dissolved in 13.4 ml of ethyl alcohol. After degassing with the sonicator, 7.05 ml of water, 8.46 ml of 0.1 M disodium phosphate buffer solution, 1.237 g of ammonium persulfate and 0.2 ml are added successively, under the conditions already indicated. of TMEDA. 4.64 g (73%) of white ester resin are obtained, giving 2.44 g of acid resin after hydrolysis and sieving. The pKa of the OH form is 5.0.
Dans les conditions du paragraphe précédent, la polymérisation est effectuée à partir de 4,653 g (0,047 mol) de N-diméthylacrylamide, 0,51 g (0,003 mol) de EBA et 0,81 g (5,16.10-3 mol) d'ester méthylique de la N-acrylyl β alanine.Under the conditions of the preceding paragraph, the polymerization is carried out from 4.653 g (0.047 mol) of N-dimethylacrylamide, 0.51 g (0.003 mol) of EBA and 0.81 g (5.16 . 10 -3 mol) of methyl ester of N-acrylyl β alanine.
Il y a formation de 4,51 g (75,75%) de résine ester sèche conduisant, après hydrolyse et tamisage, à 2,36 g de résine acide, le pKa de la forme OH est 4,7.There is formation of 4.51 g (75.75%) of dry ester resin leading, after hydrolysis and sieving, to 2.36 g of acid resin, the pKa of the OH form is 4.7.
La polymérisation est effectuée à partir de 2 g de N-diéthylacrylamide, 0,17 g de EBA et 0,32 g d'ester méthylique de la N-acrylyl alanine dans 4,5 ml d'éthanol, par additions successives de 2,35 ml d'eau, 2,82 ml de tampon au phosphate disodique 0,1 M, 0,42 g de persulfate d'ammonium et 0,067 ml de TM EDA. Après hydrolyse et tamisage, on isole 1,31 g de résine acide sèche. Le pKa de forme OH est 5,5.The polymerization is carried out from 2 g of N-diethylacrylamide, 0.17 g of EBA and 0.32 g of methyl ester of N-acrylyl alanine in 4.5 ml of ethanol, by successive additions of 2, 35 ml of water, 2.82 ml of 0.1 M disodium phosphate buffer, 0.42 g of ammonium persulfate and 0.067 ml of TM EDA. After hydrolysis and sieving, 1.31 g of dry acid resin are isolated. The pKa of OH form is 5.5.
A partir de 6 g de N-diéthylacrylamide, 0,5 g de EBA et 1,12 g de N-acrylyl ε amino caproate de méthyle dans 18,4 ml d'alcool, et par additions successives de 7,05 ml d'eau, 8,46 ml de tampon au phosphate disodique 0,1 M, 1,24 g de persulfate d'ammonium et 0,2 ml de TM EDA, on obtient, après hydrolyse et tamisage, 4,77 g de résine sèche. Le pKa de la forme OH est 5,42.From 6 g of N-diethylacrylamide, 0.5 g of EBA and 1.12 g of N-acrylyl methyl amino caproate in 18.4 ml of alcohol, and by successive additions of 7.05 ml of water, 8.46 ml of 0.1 M disodium phosphate buffer, 1.24 g of ammonium persulfate and 0.2 ml of TM EDA, 4.77 g of dry resin are obtained, after hydrolysis and sieving. The pKa of the OH form is 5.42.
A partir de 6 g de N-acrylyl hexaméthylène- imine, 0,33 g de EBA, 0,65 g d'ester méthylique de la N-acrylyl β alanine dans 8,4 ml d'alcool, on ajoute successivement dans les conditions habituelles 5,6 ml d'eau, 6,9 ml de tampon, 1,0 g de persulfate d'ammonium et 0,18 ml de TMEDA.From 6 g of N-acrylyl hexamethyleneimine, 0.33 g of EBA, 0.65 g of methyl ester of N-acrylyl β alanine in 8.4 ml of alcohol, successively added under the conditions usual 5.6 ml of water, 6.9 ml of buffer, 1.0 g of ammonium persulfate and 0.18 ml of TMEDA.
3,0 g de chlorhydrate de N-acrylyl N'-méthyl- pipérazine, 0,16 g de EBA et 0,3 g d'ester méthylique de la N-acrylyl alanine dans 4,2 ml d'éthanol sont traités successivement par 2,8 ml d'eau, 3,5 ml de tampon, 0,5 g de persulfate d'ammonium et 0,09 ml de TM EDA.3.0 g of N-acrylyl N'-methylpiperazine hydrochloride, 0.16 g of EBA and 0.3 g of N-acrylyl alanine methyl ester in 4.2 ml of ethanol are treated successively with 2.8 ml of water, 3.5 ml of buffer, 0.5 g of ammonium persulfate and 0.09 ml of TM EDA.
Dans tous ces exemples, il a été vérifié que les esters obtenus ne s'hydrolysent pas au cours de la polymérisation, les résines ne contiennent aucun CO2H libre.In all of these examples, it has been verified that the esters obtained do not hydrolyze during the polymerization, the resins contain no free CO 2 H.
On dissout 25 g (0,2 mol) de AP, 2,15 g (1,3. 10-2 mol) de méthylènebisacrylamide et 3,5 g (2,4.10-2 mol) de N-acrylyl alanine dans 57 ml d'éthanol absolu. On ajoute 30 ml d'eau puis 36 ml de tampon phosphate (pH 6,0). La solution limpide est dégazée au sonicateur 2 min. Ajouter 5,27 g de persulfate d'ammonium puis 0,88 ml de TM EDA, laisser polymériser 30 min. Le gel transparent est broyé dans un appareil Thomas, lavé à l'eau, à l'éthanol, puis à l'éther. La résine est séchée sous vide. Rdt: 27,6 g.Was dissolved 25 g (0.2 mol) of AP, 2.15 g (1.3. 10- 2 moles) methylenebisacrylamide and 3.5 g (2.4. 10 -2 mol) of N-acrylyl alanine in 57 ml of absolute ethanol. 30 ml of water are added and then 36 ml of phosphate buffer (pH 6.0). The clear solution is degassed with a sonicator for 2 min. Add 5.27 g of ammonium persulfate then 0.88 ml of TM EDA, let polymerize for 30 min. The transparent gel is ground in a Thomas apparatus, washed with water, with ethanol, then with ether. The resin is dried under vacuum. Yid: 27.6 g.
La résine est alors tamisée. On obtient la répartition en taille suivante:
Un mélange de 18,6 g (0,12 mol) de N-méthacrylylmorpholine, de 1,31 g de EBA (7,8. 10-3 mol), de 2,55 g (1,63.10-2mol) d'ester méthylique de la N-acrylyl β alanine et de 100 mg d'azo-isobutyronitrile sont ajoutés, sous azote, à une solution agitée d'alcool polyvinylique (3 g) et d'eau (250 ml). Le mélange est chauffé 3 h à 70° C. Le polymère est lavé à l'eau chaude, à l'éthanol, à l'acétone, à l'éthanol et à l'éther. Après séchage sous vide (2 mm de mercure) à 80° C, on isole 14,8 g de billes dont le diamètre est compris entre 0,1 et 0,2 mm.A mixture of 18.6 g (0.12 mol) of N-methacrylylmorpholine, 1.31 g of EBA (7.8 . 10- 3 mol), 2.55 g (1.63 . 10 -2 mol ) methyl ester of N-acrylyl β alanine and 100 mg of azo-isobutyronitrile are added, under nitrogen, to a stirred solution of polyvinyl alcohol (3 g) and water (250 ml). The mixture is heated for 3 hours at 70 ° C. The polymer is washed with hot water, ethanol, acetone, ethanol and ether. After drying under vacuum (2 mm of mercury) at 80 ° C, 14.8 g of beads, the diameter of which is between 0.1 and 0.2 mm, are isolated.
A partir d'un mélange de 18,6 g (0,12 mol) de N-méthacrylylmorpholine, de 1,31 g (7,8. 10-3 mol) d'EBA, 3,24 g (1,631 10-2 mol) d'ester méthylique de l'acide N-acrylyl ε aminocaproïque et de 100 mg d'azo-isobutyronitrile, traité dans les mêmes conditions que précédemment, on isole 12,6 g de polymère.From a mixture of 18.6 g (0.12 mol) of N-methacrylylmorpholine, 1.31 g (7.8. 10 -3 mol) of EBA, 3.24 g (1.631 10 -2 mol) of methyl ester of N-acrylyl ε aminocaproic acid and 100 mg of azoisobutyronitrile, treated under the same conditions as above, 12.6 g of polymer are isolated.
4 g (3,2 10-2 mol) d'AP, 8 g (5 10-2 mol) de N-acrylyl alanine méthyl ester et 1,2 g (7,14. 10-3 mol) d'EBA sont dissous dans 50 ml de tampon phosphate (KH2P04 0,1 M ramené à pH 6,0 avec de la soude 1 N) et 50 ml d'éthanol. A la solution limpide obtenue, on ajoute 0,6 g de persulfate d'ammonium et 0,3 ml de Span 85. Le mélange est placé dans 400 ml d'huile de paraffine, puis agité jusqu'à obtention de gouttelettes de dimension désirée. Toujours sous agitation, le milieu est désoxygéné par un bullage à l'azote de 20 min. On ajoute alors 0,92 ml de TMEDA. Après 30 min d'agitation, on dilue à l'éther de pétrole, on filtre, lave à l'éther de pétrole, à l'eau, avec un mélange eau/acétone (50/50), à l'acétone, puis à l'éther.4 g (3.2 10 -2 mol) of AP, 8 g (5 10 -2 mol) of N-acrylyl alanine methyl ester and 1.2 g (7.14 . 10- 3 mol) of ABE are dissolved in 50 ml of phosphate buffer (KH 2 P0 4 0.1 M brought to pH 6.0 with 1 N sodium hydroxide) and 50 ml of ethanol. To the clear solution obtained, 0.6 g of ammonium persulfate and 0.3 ml of Span 85 are added. The mixture is placed in 400 ml of paraffin oil, then stirred until droplets of desired size are obtained. . Still with stirring, the medium is deoxygenated by bubbling with nitrogen for 20 min. 0.92 ml of TMEDA is then added. After 30 min of stirring, diluted with petroleum ether, filtered, washed with petroleum ether, with water, with a water / acetone mixture (50/50), with acetone, then with ether.
On obtient ainsi des billes de polymère parfaitement sphériques dont on peut faire varier la taille, en ajustant la vitesse de rotation, entre 0,05 et 0,5 mm. Le rendement est voisin de 90%.Perfectly spherical polymer beads are thus obtained, the size of which can be varied, by adjusting the speed of rotation, between 0.05 and 0.5 mm. The yield is close to 90%.
La réaction peut s'effectuer également dans l'eau à la place du tampon phosphate.The reaction can also be carried out in water in place of the phosphate buffer.
Les sels de sodium des résines acides sont facilement obtenus en lavant les polymères par des solutions de soude 0,5M. On utilise 30 ml de solution de soude par millilitre de résine acide gonflée. L'excès de soude est éliminé par lavage à l'eau jusqu'à neutralité.The sodium salts of acid resins are easily obtained by washing the polymers with 0.5M sodium hydroxide solutions. 30 ml of sodium hydroxide solution are used per milliliter of swollen acid resin. The excess soda is removed by washing with water until neutral.
Les taux de gonflement des polymères ont été mesurés dans l'eau et dans différents solvants organiques. Ces mesures ont été réalisées sur des résines broyées. (Tableaux 1 et 2.)The swelling rates of the polymers were measured in water and in various organic solvents. These measurements were carried out on ground resins. (Tables 1 and 2.)
Les polyacrylamides préparés ont été testés comme échangeur de cations en chromatographie d'échange de cations sur trois substrats:
- - deux mélanges peptidiques,
- - un mélange de protéines basiques (histones provenant de thymus de veau).
- - two peptide mixtures,
- - a mixture of basic proteins (histones from calf thymus).
Les mélanges peptidiques sont composés de 2 peptides de même séquence qui ne diffèrent uniquement que par la charge:
- - Ac Gly Lys Ala Leu Arg Val 0 Me 2 charges > 0
- - Ac GLy Lys Ala Leu Arg Val OH 1 charge > 0
- - Ac Gly Lys Leu Arg Val 0 Me 2 charges > 0
- - Ac Gly Lys Leu Arg Val OH 1 charge > 0
- - Ac Gly Lys Ala Leu Arg Val 0 Me 2 charges> 0
- - Ac GLy Lys Ala Leu Arg Val OH 1 charge> 0
- - Ac Gly Lys Leu Arg Val 0 Me 2 charges> 0
- - Ac Gly Lys Leu Arg Val OH 1 charge> 0
Les séparations ont été réalisées dans un gradient de chlorure de sodium à pH constant (pH 5,0, acétate de sodium 10-2 M), en utilisant des résines tamisées correspondant aux copolymères suivants:
- - AP + MEBA + A P Ala 0 Na
- - AP + EBA + A s Cap 0 Na
- - AP + EBA + A(L) Pro 0 Na
- - AP + EBA + A Gly 0 Na
- - AP + MEBA + AP Ala 0 Na
- - AP + EBA + A s Cap 0 Na
- - AP + EBA + A (L) Pro 0 Na
- - AP + EBA + A Gly 0 Na
La taille des particules est comprise entre 0,1 et 0,25 mm. La charge en groupement carboxylique est voisine de 0,8 mEq/g de résine sèche. Les chromatogrammes, fig. 1 et 2 ci-après, montrent une très bonne séparation entre les composantes des mélanges analysés.The particle size is between 0.1 and 0.25 mm. The charge in the carboxylic group is close to 0.8 mEq / g of dry resin. The chromatograms, fig. 1 and 2 below, show a very good separation between the components of the analyzed mixtures.
Les histones de thymus de veau ont été également chromatographiées dans un gradient de chlorure de sodium (0 à 2M) (fig. 3). On observe une résolution des différentes composantes, avec un temps d'analyse très court (5 h), un débit rapide (80 ml/h), et un tampon (NaCl) mieux adapté à l'analyse par UV.Calf thymus histones were also chromatographed in a sodium chloride gradient (0 to 2M) (fig. 3). A resolution of the various components is observed, with a very short analysis time (5 h), a rapid flow rate (80 ml / h), and a buffer (NaCl) better suited to UV analysis.
Pour une résolution semblable, les chromatographies par échange d'ions d'histones sont effectuées dans des gradients aux formes élaborées de chlorure de guanidinium avec des débits très lents et des temps d'analyse qui peuvent varier entre 12 h et plusieurs jours (J. Bonner et coll., « Method in Enzymology», vol. 126; Grossmann L. et Mal- dave K. Editeurs, Academic Press, New York, 1968).For a similar resolution, histone ion exchange chromatographies are carried out in gradients with elaborate forms of guanidinium chloride with very slow flow rates and analysis times which can vary between 12 h and several days (J. Bonner et al., "Method in Enzymology", vol. 126; Grossmann L. and Maldave K. Editeurs, Academic Press, New York, 1968).
Les résines selon l'invention sont donc compatibles avec les protéines et permettent de réaliser facilement de bonnes séparations. Il est à noter de plus que les supports décrits ici admettent des débits très élevés. Il est possible de travailler jusqu'à 300 ml/h avec une colonne 1 x 25 cm.The resins according to the invention are therefore compatible with proteins and allow good separations to be easily carried out. It should also be noted that the supports described here admit very high bit rates. It is possible to work up to 300 ml / h with a 1 x 25 cm column.
Sur ces quatre figures, λ = 210 mm, la solution d'élution est 0,2M en NaCI, les numéros indiqués en abscisses sont ceux de fractions recueillies et les chiffres en ordonnées représentent la densité optique pleine échelle.
Claims (7)
from 30 to 90% by weight of a first monomer (I) defined as being the matrix and which consists of an N-acrylylpolymethyleneimine of the formula:
or an asymmetric N-acrylylaminoacid (or ester) of the L series of formula:
Priority Applications (1)
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AT82402110T ATE14890T1 (en) | 1981-11-19 | 1982-11-19 | ACRYLIC COPOLYMERS FROM N-ACRYLYLPOLYMETHYLENIMINES OR N-ACRYLYDIALKYLAMIDES, N,N'ACRYLYLDIAMINOALCANES AND NACRYLYLAMINE DUCIDES (OR ESTERS), THEIR PRODUCTION AND THEIR USE AS CATION EXCHANGER. |
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GB8134861 | 1981-11-19 | ||
GB8134861 | 1981-11-19 |
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EP0079842B1 true EP0079842B1 (en) | 1985-08-14 |
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Application Number | Title | Priority Date | Filing Date |
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EP82402109A Expired EP0081408B1 (en) | 1981-11-19 | 1982-11-19 | Ethylene diamine functional acrylic resins and preparation thereof |
EP82402110A Expired EP0079842B1 (en) | 1981-11-19 | 1982-11-19 | Acrylic copolymers based on n-acrylylpolymethylene imines or n-acrylyldialkyl amides, n,n'-acrylyldiamino alcanes and n-acrylylamino acids (or esters), their preparation and their use as cation exchangers |
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EP82402109A Expired EP0081408B1 (en) | 1981-11-19 | 1982-11-19 | Ethylene diamine functional acrylic resins and preparation thereof |
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US (2) | US4439545A (en) |
EP (2) | EP0081408B1 (en) |
JP (2) | JPS5896615A (en) |
KR (2) | KR860000559B1 (en) |
AT (2) | ATE14890T1 (en) |
AU (2) | AU553982B2 (en) |
CA (2) | CA1199448A (en) |
DE (2) | DE3276811D1 (en) |
DK (2) | DK162651C (en) |
FI (2) | FI70233C (en) |
MX (2) | MX169477B (en) |
NO (2) | NO161978C (en) |
NZ (2) | NZ202538A (en) |
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US4631327A (en) * | 1982-12-29 | 1986-12-23 | Polaroid Corporation | β-Elimination polymers useful for providing diffusion control layers in diffusion transfer photographic products |
US4683292A (en) * | 1983-08-12 | 1987-07-28 | Immunetech, Inc. | Immunotherapeutic polypeptide agents which bind to lymphocyte immunoglobulin FC receptors |
JPS60235638A (en) * | 1984-05-07 | 1985-11-22 | Mitsui Toatsu Chem Inc | Adsorptive resin |
EP0163404B1 (en) * | 1984-05-28 | 1990-06-27 | MITSUI TOATSU CHEMICALS, Inc. | Agent for absorbing and releasing water vapor |
US4691026A (en) * | 1985-07-30 | 1987-09-01 | Air Products And Chemicals, Inc. | Self- and hydroxyl reactive formaldehyde-free cyclic hemiamidal and hemiamide ketal crosslinking monomers |
US4788288A (en) * | 1985-07-30 | 1988-11-29 | Air Products And Chemicals, Inc. | Self-and Hydroxyl reactive formaldehyde-free cyclic hemiamidal and hemiamide ketal crosslinking monomers |
US4663410A (en) * | 1985-08-06 | 1987-05-05 | Air Products And Chemicals, Inc. | Polymers of self- and hydroxyl reactive formaldehyde-free cyclic hemiamidal and hemiamide ketal crosslinking monomers |
US5175254A (en) * | 1988-09-24 | 1992-12-29 | Societe D'expansion Scientifque Expansia | Solid phase peptide synthesis using a polyacrylic support in aqueous solution |
GB8822502D0 (en) * | 1988-09-24 | 1988-10-26 | Expansia Sa | New peptide synthesis method |
US5280093A (en) * | 1989-06-29 | 1994-01-18 | Rhone-Poulenc Chimie | Chiral polymers for the synthesis of pure enantiomers of amino acids |
US6031074A (en) * | 1989-08-25 | 2000-02-29 | National Institutes Of Health | Automated Peptide design and synthesis |
FR2652581B1 (en) * | 1989-10-02 | 1991-12-13 | Rhone Poulenc Chimie | METHOD FOR SOLUBILIZING PEPTIDES AND METHOD FOR SYNTHESIS OF PEPTIDES. |
US20020042377A1 (en) * | 1995-06-07 | 2002-04-11 | Steiner Joseph P. | Rotamase enzyme activity inhibitors |
US7056935B2 (en) * | 1995-06-07 | 2006-06-06 | Gpi Nil Holdings, Inc. | Rotamase enzyme activity inhibitors |
US20040221844A1 (en) * | 1997-06-17 | 2004-11-11 | Hunt Peter John | Humidity controller |
FR2791582B1 (en) * | 1999-04-02 | 2001-06-08 | Expansia Sa | USE OF AN ACRYLIC POLYMERIC SUPPORT IN SUPPORTED CATALYSIS |
AR021155A1 (en) | 1999-07-08 | 2002-06-12 | Lundbeck & Co As H | TREATMENT OF NEUROTIC DISORDERS |
FR2802121A1 (en) * | 1999-12-14 | 2001-06-15 | Expansia Sa | ORGANIC POLYMERIC SUBSTRATES WITH MONO- OR BI-DENTATE LIGANDS AND THEIR USE IN SUPPORTED CATALYSIS |
US6620939B2 (en) * | 2001-09-18 | 2003-09-16 | General Electric Company | Method for producing bisphenol catalysts and bisphenols |
US7112702B2 (en) * | 2002-12-12 | 2006-09-26 | General Electric Company | Process for the synthesis of bisphenol |
US7098253B2 (en) * | 2004-05-20 | 2006-08-29 | 3M Innovative Properties Company | Macroporous ion exchange resins |
US7683100B2 (en) * | 2005-12-21 | 2010-03-23 | 3M Innovative Properties Company | Method of making macroporous cation exchange resins |
US7674835B2 (en) * | 2005-12-21 | 2010-03-09 | 3M Innovative Properties Company | Method of making macroporous anion exchange resins |
US7674836B2 (en) * | 2006-07-28 | 2010-03-09 | 3M Innovative Properties Company | Method of making macroporous cation exchange resins |
JP2015214592A (en) * | 2012-09-11 | 2015-12-03 | 味の素株式会社 | Temperature-responsive polymer and method for manufacturing the same |
JP7135284B2 (en) * | 2017-09-29 | 2022-09-13 | 株式会社リコー | COMPOSITION, CURED PRODUCT, CONTAINER, IMAGING DEVICE, AND IMAGE FORMING METHOD |
CN110128589B (en) * | 2019-05-31 | 2021-12-03 | 上海纳米技术及应用国家工程研究中心有限公司 | Preparation method of amino acid modified microspheres and product thereof |
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US2845408A (en) * | 1954-08-04 | 1958-07-29 | Rohm & Haas | Linear polymeric amides and methods of making them |
US3069390A (en) * | 1959-07-17 | 1962-12-18 | Borden Co | Polymeric amides from polymeric acrylic acid esters and n-aminoalkyl alkanol amines and reaction products therefrom |
NL288351A (en) * | 1962-01-31 | |||
GB1108383A (en) * | 1965-12-23 | 1968-04-03 | Kodak Ltd | Acrylic polymers and light sensitive materials containing them |
JPS4948668B1 (en) * | 1971-06-26 | 1974-12-23 | ||
US3814732A (en) * | 1971-10-21 | 1974-06-04 | Hoffmann La Roche | Modified solid supports for solid phase synthesis |
NL7311320A (en) * | 1972-09-01 | 1974-03-05 | ||
FR2205538A1 (en) * | 1972-11-06 | 1974-05-31 | Ceskoslovenska Akademie Ved | Acrylate or methacrylate copolymer - useful as support for solid phase peptide synthesis |
DE2430128C3 (en) * | 1974-06-22 | 1981-11-05 | Röhm GmbH, 6100 Darmstadt | Process for the preparation of carrier-bound polypeptides |
US3965070A (en) * | 1974-10-07 | 1976-06-22 | Rohm And Haas Company | Crosslinked vinylcarbonyl resins having α-amino acid functionality |
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